History of Hydrogen Sulfide Monitoring and Control Measures Sample Clauses

History of Hydrogen Sulfide Monitoring and Control Measures. Each of the three Minnesota plants has a wastewater treatment system to prepare excess water for discharge. Wastewater comes from the beet flume, from washing the sugar beets, and from the processing of the beets to extract the sugar. The flume and beet washing operation result in the highest strength waste stream (in terms of Biological Oxygen Demand or BOD) in the wastewater system. These waste streams are sent to wastewater or mud ponds prior to treatment. These ponds can become a source of hydrogen sulfide. Both the Moorhead and East Grand Forks factories have mechanical anaerobic treatment processes to treat these wastes after their discharge to the ponds. ACS’s Crookston factory, however, relies entirely on a pond system for treatment. The air quality permits for the three Minnesota facilities require ACS to establish a hydrogen sulfide air monitoring network at each facility, and ACS has conducted such monitoring pursuant to plans approved by the MPCA since 1999. Since 1999, ACS has also invested significant funds in projects to reduce its hydrogen sulfide emissions. Expenditures for 1999-2002 are shown in Tables 1-3. Table 1 Crookston Project Finished Date Cost Pond Aeration and Dike Upgrading to improve treatment and ensure that ponds are available for storing and treating wastewater. This included cleaning out a mud pond to be used as a treatment pond. 10/30/2000 $ 1,217,245 Odor neutralizer spray system. 07/30/1999 $ 48,094 TOTAL $ 1,265,339 Table 2 East Grand Forks Project Finished Date Cost EGF Aerobic Upgrade to improve efficiency of wastewater treatment and reduce BOD. 09/01/2001 $ 2,612,090 East Grand Forks Mud Press installed to eliminate sediments going to ponds and to get rid of mud ponds that are a source of H2S. 08/31/2001 $ 4,261,486 Install an anaerobic clarifier to improve wastewater treatment efficiency. This reduces the amount of high BOD water in the ponds. 10/01/1999 $ 2,346,373 TOTAL $ 9,219,949 Table 3 Moorhead Project Finished Date Cost Waste water pumps to improve ability to treat and discharge wastewater. 08/31/2001 $ 181,824 Anaerobic clarifier to improve treatment of high BOD wastewater. 09/01/2000 $ 2,052,137 Anaerobic upgrade to improve efficiency. 08/31/2000 $ 154,507 Condenser water treatment system to reduce BOD in this pond. 07/31/2000 $ 92,432 Pond piping to improve ability to discharge and to keep treated and high BOD wastewater separated thus avoiding excessively large quantities of water that can not be discharg...
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